Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F2/00—Processes of polymerisation
  • C08F2/44—Polymerisation in the presence of compounding ingredients, e.g. plasticisers, dyestuffs, fillers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
  • C08F14/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
  • C08F14/02—Monomers containing chlorine
  • C08F14/04—Monomers containing two carbon atoms
  • C08F14/06—Vinyl chloride

Definitions

• This invention relates to a process for producing a vinyl chloride polymer characterized by polymerizing a vinyl chloride monomer in the presence of thermoplastic polyurethane. More specifically, this invention relates to a process for producing a vinyl chloride-grafted polyurethane having excellent flexibility, transparency and moldability.
• thermoplastic polyurethane and polyvinyl chloride have been used as tubes, hoses, sheets, industrial component parts, etc. in the form of a polymer blend obtained by blending these polymers in accordance with the polymer blending technique to offset the properties of the respective polymers. Since, however, the blending must be effected in a mixing device such as an extruder or a roll, it has been impossible to provide the desired inexpensive compounds. Another defect is that the polymer blend may stick to the apparatus depending upon the type of the urethane, and the resulting compound does not have satisfactory flexibility and transparency because of the insufficient dispersion of the blending components, and is not feasible in some uses.
• a vinyl chloride polymer obtained by dissolving a thermoplastic polyurethane in a vinyl chloride monomer and radical-polymerizing vinyl chloride is a molding material free from the aforesaid defects.
• a process for producing a vinyl chloride polymer which comprises dissolving a thermoplastic polyurethane soluble in a vinyl chloride monomer, particularly a thermoplastic polyurethane derived from (a) at least one long-chain glycol having a number average molecular weight of at least 500 and containing a hydroxyl group at both terminals, (b) a chain extender having a number average molecular weight of not more than 500 and (c) a polyisocyanate having an isocyanate group at both terminals, in a vinyl chloride monomer, and polymerizing the vinyl chloride monomer in the presence of a radical initiator.
• a thermoplastic polyurethane soluble in a vinyl chloride monomer particularly a thermoplastic polyurethane derived from (a) at least one long-chain glycol having a number average molecular weight of at least 500 and containing a hydroxyl group at both terminals, (b) a chain extender having a number average molecular weight of not more than 500 and (
• any type of polyurethane can be used which is soluble in a vinyl chloride monomer, and a mixing device such as an extruder or roll is not necessary.
• the polymer obtained by the process of this invention has much less stickiness, better moldability, lower hardness, greater flexibility and higher transparency than a corresponding compound obtained by the polymer blending technique.
• thermoplastic polyurethane derived from (a) at least one long-chain glycol having a molecular weight of at least 500, preferably 500 to 5000, more preferably 1000 to 2000, and containing a hydroxyl group at both terminals, (b) a chain extender having a number average molecular weight of not more than 500, and (c) a polyisocyanate having an isocyanate group at both terminals is usually employed as the thermoplastic polyurethane soluble in a vinyl chloride monomer.
• Polyurethanes containing some proportion of a hard segment may also be used if they are soluble in vinyl chloride. Polyurethanes substantially free from a hard segment are preferred.
• polyurethanes can be obtained by reacting the components (a), (b) and (c) at a mole ratio satisfying (b)/(a) ⁇ 2 and ##EQU1## preferably 0 ⁇ (b)/(a) ⁇ 2 and ##EQU2## If the mole ratio of (b)/(a) exceeds 2, the stoichiometric reaction product from the glycol and isocyanate is insoluble in the vinyl chloride monomer. In order to obtain a soluble product, the amount of the isocyanate should be adjusted to about 0.5 mole per mole of the glycol, but this polyurethane is very brittle and useless. Hence, the mole ratio of (b)/(a) ⁇ 2 is essential.
• the (b)/(a) ratio is about 0 (i.e., containing no chain extender) ⁇ (b)/(a) ⁇ 0.5. If the ratio ##EQU3## exceeds 1.1 moles, the product is insoluble in vinyl chloride. Preferably, the ratio is ##EQU4##
• the long-chain glycol having a number average molecular weight of at least 500 and containing a hydroxyl group at both terminals is preferably a linear glycol having a number average molecular weight of 500 to 5,000, i.e. polyether polyols and polyester polyols.
• polyether polyols there may be cited polyethylene glycol, polypropylene glycol, and polytetramethyene glycol. Examples also include polyteramethylene ether glycol produced from tetrahydrofuran.
• polyester polyols examples include those obtained by polycondensing at least one glycol such as ethylene glycol, 1,2-propylene glycol, 2,3-butylene glycol, 1,4-butylene glycol, 2,2'-dimethyl-1,3-propanediol, diethylene glycol, 1,5-pentamethylene glycol, diethylene glycol, 1,5-pentamethylene glycol, 1,6-hexamethylene glycol, cyclohexane-1,4-diol and cyclohexane 1,4-dimethanol with a dibasic acid such as succinic acid, maleic acid, adipic acid, glutaric acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, phthalic acid, isophthalic acid, terephthalic acid, hexahydrophthalic acid and hexahydroisophthalic acid, or the esters or acid halides of these acids.
• examples also include polylactone glycols
• copolyester polyols obtained by reacting at least two low molecular weight glycol components mixtures of these with different kinds of polyester polyols and mixtures of two or more different polyester polyols are preferred.
• Saturated aliphatic glycols having 2 to 10 carbon atoms are preferred as the chain extender (b) having a number average molecular weight of not more than 500. They are used either alone or as a mixture. Specific examples include ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 2,3-butylene glycol, 1,4-butylene glycol, 2,2'-dimethyl-1,3-propanediol, diethylene glycol, 1,5-pentamethylene glycol, 1,6-hexamethylene glycol, cyclohexane-1,4-diol, and cyclohexane-1,4-dimethanol.
• Triols and tetrols having 4 to 10 carbon atoms, and polyester polyols and polyether polyols having a molecular weight of 500 to 6,000 and containing terminal hydroxyl groups and at least one tertiary hydroxyl group in the molecular chain obtained by using the triols or tetrols may also be used in amounts which do not impair the thermoplasticity of the polyurethanes.
• triols and tetrols having 4 to 10 carbon atoms include trimethylolpropane, trimethylolethane, 1,2,3-hydroxy-2-methylpropane, 1,2,5-hydroxy-2-ethylpropane, 1,2,4-hydroxy-2-methylbutane, 1,2,5-hydroxy-2-methylpentane, 1,3,5-hydroxy-3-methylpentane, 1,3,6-hydroxy-3-methylhexane, 1,2,3,6-hydroxy-2,3-dimethylhexane, and 1,2,4,6-hydroxy-2,4-dimethylhexane, or their mixtures.
• polyisocyanate (c) Illustrative as the polyisocyanate (c) are hexamethylene diisocyanate, lysine diisocyanate, cyclohexane diisocyanate, toluidine isocyanate, 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate, 4,4'-diphenylmethane diisocyanate, p-phenylene diisocyanate, m-phenylene diisocyanate, 1,5-naphthylene diisocyanate, and mixtures of these. Of these, aliphatic diisocyanates are preferred in view of their compatibility with vinyl chloride monomer and the properties of the resulting polymer.
• a catalyst and various stabilizers can be used in the production of the thermoplastic polyurethane.
• suitable catalysts include tertiary amines such as triethylamine and triethylenediamine, nitrogen compounds such as morpholine and N-methylmorpholine, metal salts such as potassium acetate and zinc stearate, and organometallic compounds of tin or titanium, such as dibutyltin dilaurate, dibutyltin oxide and tetraisopropyl titanate.
• stabilizers against ultraviolet light such as substituted benzotriazoles, stabilizers against heat and oxidation such as phenol derivatives, and lubricants such as stearate salts or ester-type waxes in amounts which do not hamper the polymerization of vinyl chloride.
• thermoplastic polyurethane used in this invention may be produced by conventional known methods. For example, there can be used a method which comprises mixing the reagents fully in the presence, as desired, of a catalyst, casting the mixture onto a flat plate or surface, heating it, then cooling it, and pulverizing the product, a method which comprises injecting a mixture of the reagents into an extruder, and a solution reaction method which comprises reacting the reagent mixture in an organic solvent such as dimethylformamide, toluene, xylene, benzene, dioxane, cyclohexanone, methyl ethyl ketone, methyl isobutyl ketone, ethyl acetate and butyl acetate.
• an organic solvent such as dimethylformamide, toluene, xylene, benzene, dioxane, cyclohexanone, methyl ethyl ketone, methyl isobutyl ketone
• thermoplastic polyurethane soluble in vinyl chloride may be dissolved in vinyl chloride before the initiation of the reaction. Or at the start of the reaction, it may be put into a reactor together with vinyl monomer to mix them. Dissolving of the polyurethane in vinyl chloride may be effected by heating vinyl chloride or by adding a suitable amount of an organic solvent which does not affect the polymerization reaction.
• the proportion of the polyurethane to be dissolved is not more than 150% by weight, preferably 30 to 100% by weight, based on vinyl chloride.
• Vinyl chloride having dissolved therein the thermoplastic polyurethane may be polymerized by methods normally used in the production of vinyl chloride polymers, for example by suspension polymerization, emulsion polymerization, solution polymerization, bulk polymerization, precipitation polymerization, etc.
• suspension polymerization and the emulsion polymerization are preferred.
• the suspension polymerization may be carried out as follows:
• thermoplastic polyurethane and a polymerization initiator in a vinyl chloride monomer in a reaction vessel are mixed at a time with water containing a suspending agent, and the polymerization is carried out in the resulting dispersion system.
• thermoplastic polyurethane and the polymerization initiator in vinyl chloride monomer are added dropwise to water containing the suspending agent in the reactor, and the polymerization is carried out in the resulting dispersion system.
• the polymerization is carried out preferably at a temperature of 30° to 70° C.
• the polymerization initiator is a radical catalyst.
• examples include diacyl peroxides such as benzoyl peroxide and lauroyl peroxide; percarbonates such as diisopropyl peroxy dicarbonate, di-2-ethylhexyl peroxy dicarbonate and bis(4-t-butylhexyl)peroxy dicarbonate, alkyl peresters such as t-butyl peroxy pivalate, t-butyl peroxy octoate, t-butyl peroxy neodecanoate, and acetylcyclohexanesulfonyl peroxide, ketone peroxides and hydroperoxides such as cyclohexanone peroxide and t-butyl hydroperoxide and azo compounds such as ⁇ , ⁇ '-azobisisobutyronitrile and 2,2'-azobis-2,4-dimethylvaleronitrile.
• Preferred polymerization include diacy
• radical catalysts may be used singly or in combination.
• the amount of the radical catalyst is 0.01 to 5% by weight based on the vinyl chloride monomer.
• the polymerization intiator may be added dropwise to the reactant mixture at the start of the reaction, or may be added to the aqueous medium or vinyl chloride monomer solution in advance.
• the suspending agent may be any which is usually employed in suspension polymerization.
• examples include water-soluble polymeric substances such as polyvinyl alcohol, incompletely saponified polyvinyl alcohol, water-soluble cellulose ethers, a vinyl acetate-maleic anhydride copolymer and a styrene/maleic anhydride copolymer, and water-insoluble solid powders such as calcium carbonate, barium sulfate, calcium phosphate, talc and bentonite. They may be used either singly or in combination.
• an anionic surface-active agent such as fatty acid soaps, sodium alkylsulfates, sodium alkylsulfonates and sodium alkylbenzenesulfonates, and a nonionic surface-active agent such as sorbitan alkyl esters, polyoxyethylene alkyl ethers or their esters.
• the suspending agent is used in an amount of 0.01 to 5% by weight based on the monomer.
• the reactants may be fed into a reactor at a time and then polymerized as in the case of the suspension polymerization. Or it is possible to perform the polymerization reaction while adding dropwise a vinyl chloride monomer having the thermoplastic polyurethane dissolved therein in advance to a reactor containing an emulsifier, a polymerization initiator, water, etc.
• the suitable reaction temperature is about 30° to about 70° C.
• the emulsifier used in the emulsion polymerization may, for example, be one or more of anionic surface-active agents such as sodium alkylsulfonates, sodium alkylsulfates and sodium alkylbenzenesulfonates, and nonionic surface-active agents such as alkyl ethers or esters of polyoxyethylene, sorbitan alkyl esters, polyoxyethylene propylene glycol ether, higher fatty acids and higher alcohols.
• anionic surface-active agents such as sodium alkylbenzenesulfonates are used.
• Water-soluble azo compounds such as ⁇ , ⁇ '-azobisisobutyronitrile are examples of radical initiators used in this polymerization reaction.
• the amount of the radical initiator is 0.01 to 5% by weight based on the vinyl chloride monomer.
• another vinyl monomer may be copolymerized in an amount which does not impair the properties of the resulting polymer.
• the other vinyl monomer include vinyl esters, vinyl ethers, acrylic acid, methacrylic acid, alkyl esters of acrylic or methacrylic acid, maleic acid or fumaric acid, esters of maleic or fumaric acid, maleic anhydride, aromatic vinyl compounds, vinylidene halides, vinyl acetate, acrylonitrile, methacrylonitrile, and olefins such as ethylene and propylene.
• Another polymer such as an acrylic polymer, vinyl chloride polymer, a styrene polymer, or ethylene/vinyl acetate polymer, or various additives such as a dispersing aid, a stabilizer, a particle size controlling agent, a molecular weight modifier, a softening agent, a lubricant, or a coloring agent may be added before, during or after the reaction in amounts which do not adversely affect the properties of the resulting polymer.
• additives such as an acrylic polymer, vinyl chloride polymer, a styrene polymer, or ethylene/vinyl acetate polymer
• additives such as a dispersing aid, a stabilizer, a particle size controlling agent, a molecular weight modifier, a softening agent, a lubricant, or a coloring agent may be added before, during or after the reaction in amounts which do not adversely affect the properties of the resulting polymer.
• the polymers obtained by the process of this invention are graft copolymers which are flexible at room temperature without any particular need to add a plasticizer.
• the mixed polyol was well mixed with 100 ppm of tin octenoate.
• the mixture was rapidly mixed and stirred with 5.05 moles of hexamethylene diisocyanate (HDI for short) heated in advance at 40° C.
• the mixture was taken out onto a vat.
• the vat was heated at 160° C. for 30 minutes and then at 80° C. for 16 hours to give a thermoplastic polyurethane [A].
• the polyurethane obtained was soluble in toluene.
• a solution of the polyurethane in methyl ethyl ketone to a solids content of 20% by weight had a viscosity of 300 cps.
• the mixture was well mixed with 200 ppm of tetraisopropyl titanate.
• 2.94 moles of HDI kept at 40° C. was added.
• the mixture was worked up in the same way as in Synthesis Example 1 to give a thermoplastic polyurethane [B].
• the polymer was soluble in toluene.
• the polymer was soluble in toluene.
• thermoplastic polyurethanes [A], [B], and [C] obtained in Synthesis Examples 1 to 3, vinyl chloride polymers in accordance with this invention were produced.
• thermoplastic polyurethanes 1,000 parts of vinyl chloride monomer and 3 parts of ⁇ , ⁇ '-azodiisobutyronitrile, and at room temperature, they were stirred for 3 hours to dissolve the polyurethane. Then, 5 parts of polyvinyl alcohol and 3,500 parts of water were introduced. The mixture was heated to 60° C., and polymerized for 15 hours. The resulting product in suspension was dried under vacuum at 40° C. to give a powdery polymer.
• the sheet was prepared as follows: A mixture of 100 parts of the polymer, 3 parts of epoxidized soybean oil, 1 part of calcium stearate and 1 part of zinc stearate was kneaded on a roll at 150° C. for 10 minutes, and then pressed at 170° C. for 5 minutes.
• P polyvinyl chloride
• thermopolastic polyurethane [A] obtained in Synthesis Example 1 1,000 parts of vinyl chloride monomer, 3,500 parts of water, 3 parts of ⁇ , ⁇ '-azodiisobutyronitrile (polymerization initiator) and 5 parts of polyvinyl alcohol (dispersing agent), and the mixture was stirred at room temperature for 3 hours to dissolve the polyurethane, and then polymerized at 60° C. for 15 hours.
• the resulting product in suspension (1425 parts; 95%) was dried in vacuum at 40° C. to give a powdery polymer.
• a moisture of 100 parts of the resulting polymer, 3 parts of epoxidized soybean oil, 1 part of calcium stearate and 1 part of zinc stearate was kneaded on a roll at 150° C. for 10 minutes, and pressed at 170° C. for 5 minutes.
• the properties of the resulting sheet were determined, and the results are shown in the following table.

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• 1981
  • 1981-08-28 JP JP56134050A patent/JPS5837019A/ja active Granted
• 1982
  • 1982-08-24 US US06/410,964 patent/US4672095A/en not_active Expired - Fee Related
  • 1982-08-27 DE DE19823231992 patent/DE3231992A1/de active Granted

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